Polyethylene composition

ABSTRACT

The invention relates to polyethylene compositions containing 85-99.5 weight % of component A, which is a linear (co)polymer of ethylene having a bimodal weight distribution, and 0.5-15 weight % of component B having a unimodal molecular weight distribution. Component A is 40-60% by weight of a low molecular weight component (A1) having a weight average molecular weight between 5,000 and 50,000 g/mol, and a molecular weight distribution Mw/Mn between 2.5 and 9 and 60-40% by weight of a high molecular weight component (A2) having a weight average molecular weight between 300,000 and 900,000 g/mol, and a molecular weight distribution M/w/Mn between 4.5 and 12. Component B is a linear ethylene polymer having a molecular weight between 150,000-600,O00 g/mol and an average molecular weight which is higher than the average molecular weight of component (A1) but lower than the average molecular weight of component (A2) and a density controlled within the range of 910-960 kg/m 3 . Component B is produced separately from component A by using Ziegler-Natta or metallocene catalysts.

BACKGROUND OF THE INVENTION

The invention concerns polyethylene compositions having improved physical properties. Particularly the invention concerns polyethylene compositions, which are prepared from several components and which are suitable for manufacturing tough pipe materials and cable isolation materials having good stress cracking resistance, film grades having good appearance and low gel content, and blown products such as bottles.

Generally the strength properties of polyethylene materials depend on molecular weight. The greater the molecular weight is the greater are elasticity, stiffness and creep properties. In products having very high molecular weight the processability properties are degraded in such degree that the manufacturing of end products becomes problematic.

One way to manufacture polyethylene grades more suitable to different applications is to form the polyethylene composition from several different components having different molecular weight distributions. Such method is disclosed in U.S. Pat. No. 4,336,352, in which the composition is formed from three different components prepared by a process comprising several stages, or in separate processes, in which the product thereof are melt mixed together to achieve the end product. According to the method the end product is formed from component (A) having a molecular weight between 1000-100,000, component (B) having a molecular weight between 100,000-1,000,000 and component (C) having a molecular weight between 400,000-6,000,000. The amount of component (C) in the end product is between 1-10 percent by weight. In other words, the idea of the method according this publication is that to the mixture of two components having different molecular weight is added a minor amount (1-10%) of a polyethylene having a very high molecular weight.

In EP-publication 129312 there is disclosed another similar polyethylene composition having three components, in which the product is formed from component (A) having a molecular weight between 50,000-500,000, component (C) having a molecular weight between 100,000-1,500,000 and component (B) having a molecular weight between 50,000-500,000 and being a homopolymer produced by a chromium catalyst. Components (A), (B) and (C) can be according to the publication manufactured as separate components or components (A) and (C) can together form a product prepared by a two-phase method, in which the weight ratio between components (A) and (A) is between 70:30-30:70. In the latter case the product can thus be considered a mixture formed from a unimodal product (B) and bimodal product (A/C).

A similar product formed from three components is disclosed also in U.S. Pat. No. 4,230,831. In this case the third component is low density polyethylene, which is produced by high pressure process. It has different, more branched structure compound compared to polyethylenes produced in low pressure process. In this way it is not possible to obtain good ESCR-values.

In EP-publication 517222 it has also been disclosed a polyethylene product formed from an unimodal component and a bimodal component, which have been melt mixed together. In this case the product has been formed from 50-80 percent by weight of very high density polyethylene having a very broad molecular weight distribution, and from 20-50 percent by weight of LLD polyethylene or LD polyethylene having a melt index MFR₂ between 0.5-2, and the product obtained is presented to be suitable for manufacturing pipes, sheets and films for low temperature conditions.

The addition of component having very high molecular weight, as disclosed in U.S. Pat. No. 4,336,352 decrease the homogenity of the product by causing gels and makes the end product more stiff and thereby the processing more difficult.

The addition of homopolymer to bimodal polymer, as suggested in EP-publication 129,312, has been found to impare the stress cracking resistance of the end product.

In bimodal products prepared by multiphase polymerization and containing low molecular weight polyethylene and high molecular weight polyethylene the processability can be essentially improved and molecular weight distribution can be controlled within a broad range. However, it has been found according to the invention that it is possible in certain way to improve the mixing of two phases having very different molecular weights and thereby the morphology and the processabily of the products and the optimization of the mechanical properties. When essential improvements in processability and mechanical properties are tried to achieve, the phases of bimodal product have to be very different. This requires very accurate control of the phases.

SUMMARY OF THE INVENTION

The invention is based on finding that the optimization of comonomer distribution in the molecular weight distribution area between the both main components of the bimodal product is important. In this area even a small amount of certain third component causes considerable improvements in the properties of the end product. Especially it has been found according to the invention that addition of comonomer to the middle of molecular weight distributions of the components of the bimodal composition affects essentially on certain properties. In addition, an addition made to a middle of the molecular weight area improves the miscibility of the bimodal product thereby increasing the homogenity of the end product.

Thus the invention concerns a polyethylene composition, which contains 85-99 percent by weight of a component (A) having a bimodal molecular weight distribution and a component (B) having an unimodal molecular weight distribution. Component (B) is a linear ethylene polymer having molecular weight between 150,000-600,000, a molecular weight distribution between 3.5-9.5, a melt index MFR₂₁ between 0.5-10 and a density controlled within the range of 910-960 kg/m³, and the amount of component (B) calculated from the end product is between 1-15 percent by weight. The melt flow indices described herein have been determined at 190° and the units are expressed as "g/10 min". MFR₂, has been determined under a 21.6 kg load.

The polyethylene composition according to the invention is thus formed from two main components, the bimodal component of which has a bimodal molecular weight distribution. This component has the following general properties:

    ______________________________________                                                density     940-955 kg/m.sup.3                                                 M.sub.W     150,000-400,000                                                    M.sub.W /M.sub.n                                                                           15-35                                                              MFR.sub.2   0.03-0.6                                                    ______________________________________                                    

The bimodal component is formed of a which is a low molecular weight fraction having preferably a molecular weight of 5000-50,000, a molecular weight distribution M_(w) /M_(n) of 2.5-9 and melt index MFR₂ between 10-1000 g/10 min and a density between 950-980 kg/m³. Most preferably this component has relatively high density, preferably 950-980 kg/m³ and high melt flow MFR₂, preferably 150-500. The proportion of the fraction from the whole bimodal component is preferaby 40-60%. The another fraction of the bimodal component comprises a fraction having a calculated molecular weight M_(w) of 300,000-900,000 and a molecular weight distribution of 4.5-12. The proportion of this fraction of the whole bimodal component is preferaby 60-40%. The calculated molecular weight is achieved for example by calculating from the molecular weight distribution of the low mole mass fraction and the molecular weight distribution the bimodal weight product measured by gel permeability.

The bimodal component is prepared preferably by a two-step process, in which in the first polymerization step the low molecular weight fraction is formed and in the second step polymerization is continued in another reactor to prepare the bimodal product. According to the invention it is also possible to form the high molecular weight component in the first reactor and the low molecular weight component in the second reactor.

It is especially preferable to prepare the bimodal component by a two-phase process, in which the first step is formed of a loop reactor in which ethylene is polymerized in propane medium and in which the second step is formed of a gas-phase reactor. However, both phases can be slurry polymerizations or gas phase polymerizations.

The other main component in the polyethylene composition according to the invention is a linear ethylene polymer having an unimodal molecular weight distribution and having a molecular weight preferably between 150,000-600,000, a molecular weight distribution between 3.5-9.5 and a melt index MFR₂₁, between 0.5-10. The density of the component is controlled so that it is between 910-960 kg/m³. According to the invention it has been found that the density of the unimodal component being higher than 950 kg/m³ the stress cracking resistance of the end product becomes essentially lower.

Thus, this component can be in the vicinity of the upper limit of the density area also an ethylene homopolymer, whereby improvements especially in the homogenity and creep properties are achieved and thus the end products are suitable, among others, for the manufacturing of films.

According to the most preferable embodiment of the invention the unimodal component is however a linear ethylene copolymer, the density of which is controlled by adding in the polymerization as comonomer C₄ -C₈ alphaolefins such amount that the density of the component is within the range of 910-950 kg/m³, preferably within the range of 920-945 kg/m³. According to the invention it has been found that already minor amounts of such copolymer component added to the described bimodal component optimize the comonomer distribution and molecular weight distribution of the mixture, whereby the stress cracking properties of the mixture improve considerably. Thus, according to the invention the amount of the copolymer component calculated from the end product is between 1-15 percent by weight, preferaby between 2-12 percent by weight.

The comonomer used in the formation of the copolymer can be any C₄ --C₄ alphaolefin or mixture thereof. Thus the comonomer can be selected for example from the group of 1-butene, 1-hexene, 4-methyl-1-pentene, 1-octene or the mixtures thereof. The amount of the comonomer in the copolymer can be selected between 0.5-10 weight-%.

The unimodal component B can be prepared by any suitable method, for example by slurry polymerization or gas phase polymerization. As catalyst any kind of Ziegler-Natta type catalyst, chromium catalyst or metallocene catalyst can be used together with conventional cocatalysts.

The polyethylene composition according to the invention can be prepared also by a multi-phase polymerization, in which for example in the first step an unimodal component is formed in amount corresponding of 1-15 weight-% of the end product and the bimodal component is formed in the second and the third polymerization step.

If the bimodal component and the copolymer component is prepared separately, the mixing of them together is carried out preferably by melt-mixing in an extruder, which can be any model giving an efficient mixing.

Further the polyethylene composition according to the invention can be prepared also so that a part of the fraction included in the low molecular weight fraction is added separately into the mixture formed by the bimodal component and unimodal component. The mixing is carrried out preferaby in an extruder, where the bimodal component and the unimodal polymer component are added in the beginning and a part, for example 1-50 weight-% of the component of low molecular weight is added as a side feed of the extruder. In this way it can be improved the homogenity of the end product in the way described in Finnish patent application FI931343.

DETAILED DESCRIPTION OF THE INVENTION

The invention is described further by examples. The stress cracking resistance (ESCR) is measured with CTL (constant tensile load) test by using the strain of 5.5 MPa. In the method it is followed the advance of the crack in pre-notched standard sample bar. The result is described as the time (h) required to the breaking of the test bar.

EXAMPLE 1

A bimodal polyethylene component A was prepared by a two-step process, in which the first step consisted of a loop polymerization and the second step consisted of a gas phase polymerization. The production rate of the loop reactor was 35-40 kg/h and the production rate of the gas phase reactor was the same. As a catalyst a Ziegler-Natta catalyst was used prepared according to Finnish patent application FI916192 by using Al-alkyl as cocatalyst. The catalyst was fed only into the loop reactor.

The polymerization conditions were the following:

    ______________________________________                                         Loop reactor                                                                   Reactor temperature   95° C.                                            Reactor pressure      65 bar                                                   Ethylene feed rate    35-40 kg/h                                               Hydrogen feed rate    50-60 g/h                                                Medium (diluent)      propane                                                  Gas phase reactor                                                              Reactor temperature   75° C.                                            Reactor pressure      20 bar                                                   Ethylene feed rate    50-60 kg/h                                               Hydrogen feed rate    15-20 g/h                                                Comonomer feed rate   2, 8 kg/h                                                ______________________________________                                    

The high density (974 kg/m³) polymer fraction manufactured in the loop reactor was introduced into the gas phase reactor, in which polymerization was continued for manufacturing a bimodal product. The ratio between fractions produced in the loop reactor and in the gas phase reactor were 51:49-52:48. The properties of the product are presented in Table 1A.

Copolymer components B1-B2 having different densities were prepared by using the same catalyst as in the case of component A in the gas phase reactor, where the reaction conditions were the following:

    ______________________________________                                         Production rate        10 kg/h                                                 Reactor pressure       18 bar                                                  Reactor temperature    90° C.                                           Hydrogen partial pressure                                                                             0.7-0.8 bar                                             Ethylene partial pressure                                                                             7.5 bar                                                 Comonomer              butene                                                  Butene partial pressure                                                                               0.35-0.4 bar                                            ______________________________________                                    

Component B3 was a commercial ethylene copolymer NCPE (Borealis N.V) manufactured by chromium catalyst and having a density of 952 kg/m³.

The properties of components B1-B3 are disclosed in Table 1B.

                  TABLE 1A                                                         ______________________________________                                                Reactor                          Density                                Fraction                                                                              split    MFR.sub.5                                                                               MFR.sub.21                                                                            FRR21/5 kg/m.sup.3                             ______________________________________                                         A1     51:49    0, 42    9, 5   22, 6   948                                    A2     52:48    0, 42    10     23, 8   948                                    A3     51:49    0, 43    9, 1   21, 2   947, 9                                 ______________________________________                                    

                  TABLE 1B                                                         ______________________________________                                                Comomer                          Density                                Fraction                                                                              content (%)                                                                              MFR.sub.21                                                                             M.sub.W  × 1000                                                                   M.sub.W /M.sub.n                                                                     kg/m.sup.3                             ______________________________________                                         B1     8, 2      2       308      7, 2  910                                    B2     2, 0      2, 5                   933                                    B3     --        2       256      12    952                                    ______________________________________                                    

Components A and B were melt-mixed together in an extruder (ZSK-30, Werner-Pfleiderer). The revolution speed of the screw was 200 rpm and the production rate of the extruder was 6 kg/h. The temperature of the melt was 210-200° C. As stabilization agent 2500 ppm of Irganox B225 was added.

The properties of the products are presented in the following Table C.

                                      TABLE 1C                                     __________________________________________________________________________                                         ESCR                                                                Density                                                                            ESCR (h)                                                                              Elongation                                 Experiment                                                                           Fractions                                                                           Composition                                                                          MFR.sub.5                                                                          MFR.sub.21                                                                         kg/m.sup.3                                                                         CTL/5.5 MPA                                                                           mm/100/°                            __________________________________________________________________________     1     A1   100.0 0.42                                                                               9.5 948 400                                               2     A2   100:0 0.42                                                                               10  948 500                                               3     A3 + B1                                                                             95:5  0.37                                                                               8   947 980    5.4/5.7                                    4     A3 + B2                                                                             95:5  0.32                                                                               6.8 948 850    3.5/3.0                                    5     A3 + B3                                                                             95:5  0.35                                                                               8.2 950 270    2.7/2.7                                    __________________________________________________________________________

The results indicate that with the compositions according to the invention it could be further improve ESCR-values compared with the only bimodal compositions in comparative tests 1 and 2. In experiment 5 into the bimodal polyethylene was added a homopolymer, which had been prepared by using chromium catalyst and the density of which was relatively high, e.g. 952 kg/m³. Also in this case the ESCR-value was essentially worse than the compositions according to the invention. The best stress cracking properties were achieved in experiment 5, in which a homopolymer was used.

EXAMPLE 2

According to Example 1 a bimodal polyethylene was prepared so that the polymer fraction produced in the loop reactor having a high density (975 kg/m³) and a high melt flow (MFR₂ =405) was introduced into a gas phase reactor in which the polymerization was continued for manufacturing bimodal product. 1-Butene was added into gas phase reactor as comonomer. The ratio between the components produced in the loop reactor and in the gas phase reactor was 50:50. The bimodal polyethylene obtained had the following properties:

    ______________________________________                                                MFR.sub.5     0.34                                                             MFR.sub.21    9                                                                FFR.sub.21/5  26.5                                                             M.sub.W       281,000                                                          M.sub.W /M.sub.n                                                                             21, 3                                                            Density       951.1 kg/m.sup.3                                                 Comonomer     about. 1.4%                                                      content                                                                 ______________________________________                                    

Likewise according to Example 1 it was prepared an ethylene-butene copolymer B4 having a density of 937 kg/m³, MFR₂₁, of 4, a molecular weight M_(w) of 237,000 and M_(w) /M_(n) of 6.1. The amount of comonomer in the copolymer was 1.1 weight-%

Components A and B were melt-mixed in the extruder according to Example 1. The properties of the products are presented in the following Table 2.

                                      TABLE 2                                      __________________________________________________________________________                    Co-                       ESCR                                             Compo                                                                              monomer       M.sub.w Density                                                                            (h)                                   Experiment                                                                           Fractions                                                                           sition                                                                             content (%)                                                                          MFR.sub.5                                                                          MFR.sub.21                                                                         (×1000)                                                                      M.sub.w /M.sub.n                                                                   kg/m.sup.3                                                                         CTL/5.5 MPa                           __________________________________________________________________________     6     A4   100:0                                                                              1.4   0.34                                                                               9   281 21.3                                                                               951.1                                                                              1125                                  7     A4 + B4                                                                             98:2                                                                               1.4           274 25.5    1280                                  8     A4 + B4                                                                             95:5                                                                               1.4   0.34                                                                               8   274 27.1                                                                               950.5                                                                              1120                                  9     A4 + B4                                                                              90:10                                                                             1.3   0.35                                                                               6.8 277 27.1                                                                               950 2190                                  __________________________________________________________________________

Due to greater melt flow index (MFR₂) of the polymer fraction prepared in the loop reactor the ESCR-values of the end products were at higher levels as in Example 1. In spite of that the results indicate that when adding medium density copolymer it was achieved an essential improvement in the ESCR-values of the end product the addition amount being 10 weight-%.

COMPARISON EXAMPLE 1

According to Example 1 it was manufactured bimodal polymer so that the polymer fraction produced in the loop reactor and having a high density (975 kg/m³) and high melt flow index (MFR₂ =450) was introduced into a gas phase reactor where the polymerization was continued for manufacturing a bimodal product. The ratio between the fractions produced in the loop reactor and in the gas phase reactor were 50:50. The bimodal product A5 obtained had the following properties:

    ______________________________________                                                MFR.sub.5     0.39                                                             MFR.sub.21    10.4                                                             FRR21/5       26.7                                                             Density       949 kg/m.sup.3                                            ______________________________________                                    

An ethylene homopolymer B5 was prepared in the same way as component B4 in Example 2, but without comonomer addition. The properties of the product were as follows:

    ______________________________________                                                 MFR.sub.21   4.0                                                               M.sub.W      254,000                                                           M.sub.W /M.sub.n                                                                            8.5                                                               Density      958 kg/m.sup.3                                            ______________________________________                                    

Components A and B were melt-mixed in an extruder in various conditions. The properties of the products obtained are presented in the following Table 3.

                                      TABLE 3                                      __________________________________________________________________________                Compo       M.sub.W Density                                                                            ESCR (h)                                    Experiment                                                                           Fractions                                                                           sition                                                                             MFR.sub.5                                                                          MFR.sub.21                                                                         (×1000)                                                                      M.sub.W /M.sub.n                                                                   kg/m.sup.3                                                                         CTL/5, 5 MPa                                __________________________________________________________________________     11    A5   100:0                                                                              0, 39                                                                              10, 4                                                                              253 19, 9                                                                              949 910                                         12    A5 + B5                                                                             98:2                                                                               0, 37                                                                              9, 65       949 662                                         13    A5 + B5                                                                             95:5                                                                               0, 33                                                                              7, 93       949 695                                         14    A5 + B5                                                                             90:10                                                                              0, 33                                                                              7, 45                                                                              278 19, 9                                                                              950 377                                         15    A5 + B5                                                                             85:15                                                                              0, 34                                                                              7, 56       950 142                                         __________________________________________________________________________

The results clearly indicate that when adding homopolymer having a density above 950 kg/m³ to the bimodal product the ESCR-properties do not improve, but actually worsen, the more the addition amount. 

We claim:
 1. A polyethylene composition comprising 85-99.5 weight-% of component A, which is a linear (co)polymer of ethylene having a bimodal molecular weight distribution, comprising:40-60% by weight of a low molecular weight component (A1) having a weight average molecular weight between 5,000 and 50,000 g/mol, and a molecular weight distribution Mw/Mn between 2.5 and 9; and 60-40% by weight of a high molecular weight component (A2) having a weight average molecular weight between 300,000 and 900,000 g/mol, and a molecular weight distribution Mw/Mn between 4.5 and 12; and 0.5-15 weight-% of component B having a unimodal molecular weight distribution and a molecular weight between 150,000 and 600,000 g/mol, said component B having an average molecular weight which is higher than the average molecular weight of said component (A1) but lower than the average molecular weight of said component (A2), and a density controlled within the range of 910-960 kg/m³, said component B being produced separately from said component A by using Ziegler-Natta or metallocene catalysts.
 2. A polyethylene composition according to claim 1, wherein the melt flow index determined under a 21.6 kg load or MFR₂₁ of said component B is between 0.5 and 10 g/10 min.
 3. A polyethylene composition according to claim 1, characterized in that said component B is a linear ethylene copolymer having a density controlled by adding in the polymerization as comonomer C₄ -C₈ alphaolefins in such amount that the density of said component B is within the range of 910-950 kg/m³.
 4. A polyethylene composition according to claim 3, characterized in that said comonomer is selected from the group consisting of 1-butene, 1-hexene, 4-methyl- 1-pentene, 1-octene and mixtures thereof.
 5. A polyethylene composition according to claim 1, wherein said bimodal Component A is formed of a first subcomponent, having a molecular weight between 5,000-50,000, a molecular weight distribution M_(w) /M_(n) between 2.5-9 and a melt flow index determined under a 2.6 kg load or MFR₂ between 10-1,000 g/10 min, and a second subcomponent having a calculated molecular weight M_(W) between 300,000-900,000 and a molecular weight distribution between 4.5-12.
 6. A polyethylene composition according to claim 5, characterized in that the melt flow index determined under a 2.16 kg load or MFR₂ of said first subcomponent is between 150-500 g/10 min, and the density is between 950-980 kg/m³.
 7. A polyethylene composition according to claim 1, characterized in that said component B comprises 0.5-10 weight-% of comonomer.
 8. A polyethylene composition according to claim 1, characterized in that said components A and B are melt-mixed together.
 9. A polyethylene composition according to claim 5, characterized in that said composition is prepared by adding 1-50 weight-% of said first subcomponent to the mixture of components A and B.
 10. A polyethylene composition according to claim 9, characterized in that said composition is prepared by mixing together components A and B in an extruder and adding at least part of the component of said first subcomponent through a side feed to said extruder.
 11. A polyethylene composition according to claim 1, characterized in that said polyethylene composition has the following properties:

    ______________________________________                                                density     930-960 kg/m.sup.3                                                 M.sub.W     120,000-400,000                                                    M.sub.W /M.sub.n                                                                           7-45                                                               MFR.sub.2   0.02-1.0                                                    ______________________________________                                    


12. A polyethylene composition according to claim 1, characterized in that component A is prepared by a loop-gas phase reactor combination with Ziegler-Natta catalyst.
 13. A polyethylene composition according to claim 5, characterized in that said first subcomponent is prepared in a loop reactor by using propane as a medium.
 14. A polyethylene composition according to claim 1, characterized in that components A and/or B are prepared by polymerizing ethylene in the presence of a catalyst selected from the group consisting of a Ziegler-Natta, chromium or metallocene catalyst.
 15. The polymer composition of claim 1, wherein said component B is a linear ethylene polymer.
 16. The polymer composition of claim 1, wherein said component B has a molecular weight distribution between 3.5 and 9.5. 